References of "Toye, Dominique"
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See detailVALIDATION OF AN EULER-LAGRANGE COMPARTMENT MODEL FOR THE DESIGN OF SCALE-DOWN BIOREACTOR USED IN ANIMAL CELL CULTURES
Delafosse, Angélique ULiege; Calvo, Sébastien ULiege; Collignon, Marie-Laure ULiege et al

in Proceeding of the 15th European Conference on Mixing (2015, June)

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See detailCatalytic epuration of biogaz
Claude, Vincent ULiege; Toye, Dominique ULiege; Heinrichs, Benoît ULiege et al

Poster (2015, May 08)

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See detailA fungal biofilm reactor based on metal structured packing improves the quality of a Gla::GFP fusion protein produced by Aspergillus oryzae
Zune, Quentin ULiege; Delepierre, Anissa ULiege; Gofflot, Sebastien et al

in Applied Microbiology and Biotechnology (2015)

Fungal biofilm is known to promote the excretion of secondary metabolites in accordance with solid-state related physiological mechanisms. This work is based on the comparative analysis of classical ... [more ▼]

Fungal biofilm is known to promote the excretion of secondary metabolites in accordance with solid-state related physiological mechanisms. This work is based on the comparative analysis of classical submerged fermentation with a fungal biofilm reactor for the production of a Gla::GFP fusion protein by Aspergillus oryzae. The biofilm reactor comprises a metal structured packing allowing the attachment of the fungal biomass. Since the production of the target protein is under the control of the promoter glaB, specifically induced in solid-state fermentation, the biofilm mode of culture is expected to enhance the global productivity. Although production of the target protein was enhanced by using the biofilm mode of culture, we also found that fusion protein production is also significant when the submerged mode of culture is used. This result is related to high shear stress leading to biomass autolysis and leakage of intracellular fusion protein into the extracellular medium. Moreover, 2D-gel electrophoresis highlights the preservation of fusion protein integrity produced in biofilm conditions. Two fungal biofilm reactor designs were then investigated further, i.e. with full immersion of the packing or with medium recirculation on the packing, and the scale-up potentialities were evaluated. In this context, it has been shown that full immersion of the metal packing in the liquid medium during cultivation allows for a uniform colonization of the packing by the fungal biomass and leads to a better quality of the fusion protein. [less ▲]

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See detailHighly efficient, long life, reusable and robust photosynthetic hybrid core-shell beads for the sustainable production of high value compounds
Desmet, Jonathan; Meunier, Christophe; Danloy, Emeric et al

in Journal of Colloid & Interface Science (2015), 448

An efficient one-step process to synthesize highly porous (Ca-alginate–SiO2–polycation) shell: (Na-alginate– SiO2) core hybrid beads for cell encapsulation, yielding a reusable long-life ... [more ▼]

An efficient one-step process to synthesize highly porous (Ca-alginate–SiO2–polycation) shell: (Na-alginate– SiO2) core hybrid beads for cell encapsulation, yielding a reusable long-life photosynthetically active material for a sustainable manufacture of high-value metabolites is presented. Bead formation is based on crosslinking of an alginate biopolymer and mineralisation of silicic acid in combination with a coacervation process between a polycation and the silica sol, forming a semi-permeable external membrane. The excellent mechanical strength and durability of the monodispersed beads and the control of their porosity and textural properties is achieved by tailoring the silica and alginate loading, polycation concentration and incubation time during coacervation. This process has led to the formation of a remarkably robust hybrid material that confers exceptional protection to live cells against sheer stresses and contamination in a diverse range of applications. Dunaliella tertiolecta encapsulated within this hybrid core–shell system display high photosynthetic activity over a long duration (>1 year). This sustainable biotechnology could find use in high value chemical harvests and biofuel cells to photosynthetic solar cells (energy transformation, electricity production, water splitting technologies). Furthermore the material can be engineered into various forms from spheres to variable thickness films, broadening its potential applications. 2015 Elsevier Inc. All rights reserved. [less ▲]

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See detailCFD Large Eddy Simulation of the hydrodynamics of stirred mini-bioreactors operating with stem cell culture mixing conditions
Collignon, Marie-Laure ULiege; Martin, Céline; Toye, Dominique ULiege et al

Poster (2015, January 18)

The expansion of hMSC adhered on microcarriers is a proven technology to allow the production of quantitatively (cell density and growth rate) and qualitatively (preservation of cell stemness) the amounts ... [more ▼]

The expansion of hMSC adhered on microcarriers is a proven technology to allow the production of quantitatively (cell density and growth rate) and qualitatively (preservation of cell stemness) the amounts of cells required for clinical applications. In that context of process optimization, a platform of 6 parallel 250 mL stirred minibioreactors have been designed and fully equipped for hMSC cultivation on microcarriers. The local hydrodynamics in these bioreactors have been characterized using CFD simulations and experimental measurements. GOALS: 1) Evaluation of the flexibility of the platform for extensively studying the coupling between hydrodynamics and hMSC physiological response (growth, stemness) by changing agitation conditions. 2) Evaluation of the scale down ability of platform as prediction tool of the hMSC behavior in larger bioreactor scale. [less ▲]

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See detailHYDRODYNAMICS IN A DISPOSABLE RECTANGULAR PARALLELEPIPED STIRRED BIOREACTOR WITH ELLIPTIC PENDULUM MOTION PADDLE
Collignon, Marie-Laure ULiege; Droissart, Laurent; Delafosse, Angélique ULiege et al

in Biochemical Engineering Journal (2015), 93

Stainless steel bioreactors increasingly fall behind to their disposable counterparts in pharma research as they do not require cleaning or sterilization. This led company ATMI LifeSciences to develop the ... [more ▼]

Stainless steel bioreactors increasingly fall behind to their disposable counterparts in pharma research as they do not require cleaning or sterilization. This led company ATMI LifeSciences to develop the “Nucleo™”. Original in design, this disposable bioreactor comprises a rectangular parallelepiped plastic bag stirred by a paddle revolving in elliptic pendulum motion. Studies covering this bioreactor showed good homogeneity of culture medium as well as good productivity for animal cell cultures. To further explain these good performances, the flow inside the “Nucleo™” had to be resolved. This paper focuses on the mean flow description, computed from stereo-PIV measurements performed in 20 verticals covering the whole volume of a 50 dm3 Nucleo™ bioreactor. As the flow is already turbulent in the chosen agitation conditions, its dimensionless mean velocity field does not vary with the paddle rotational speed. Mean flow pattern exhibits an axial symmetry – same flow is observed in opposite quarters of the tank – and can be described as a three-dimensional helix coiled on itself to form a distorted horizontal torus which covers the whole tank volume. Mean velocity value is on average doubled in the cone swept by the paddle, and its two horizontal components are twice higher than its vertical ones. However, mean velocity remains significant everywhere and, in particular, no stagnant area is observed in tank corners. Our results thus confirm previous studies observations. [less ▲]

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See detailPositive operations on convective drying of sewage sludge: comparison of back mixing and sawdust addition
Li, Jie; Fraikin, Laurent ULiege; Salmon, Thierry ULiege et al

in Proceedings of the 5th European Drying Conference (EuroDrying'2015) (2015)

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See detailEffect of sawdust addition on convective drying of sludges: comparison of the structural characteristics
Li, Jie; Plougonven, Erwan ULiege; Fraikin, Laurent ULiege et al

in Proceedings of the 5th European Drying Conference (EuroDrying'2015) (2015)

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See detailInvestigation on Convective Drying of Mixtures of Sewage Sludge and Sawdust in a Fixed Bed
Li, Jie ULiege; Fraikin, Laurent ULiege; Salmon, Thierry ULiege et al

in Drying Technology (2015), 33(6), 704-712

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See detailRedistribution of a mixture of organic vapours inside a activated carbon filter
Berezovka, Inna; Hichem, Fettaka; Salmon, Thierry ULiege et al

in Chemical Engineering Journal (2015), 280

X-ray tomography in a combination with gas chromatography was used for quantitative and qualitative analysis of adsorption front of organics distributed inside activated carbon filters during defined ... [more ▼]

X-ray tomography in a combination with gas chromatography was used for quantitative and qualitative analysis of adsorption front of organics distributed inside activated carbon filters during defined period of storage. This approach was tested against filters partly contaminated by CCl4 and n-heptane separately and by their mixture. X-ray tomography was shown to be capable to “recognize” different organic vaporvapours adsorbed on activated carbon and to follow their movement inside filters. Gas Chromatography was used either to monitor all possible losses of adsorbed species spices from the carbon bed, or either for “seeing” the location of each component of the mixture of organics along the filter depth. Such in situ information could be useful for evaluation of lifetime of carbon filters and for a thorough understanding of adsorption process taking place under static conditions. [less ▲]

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See detailImage analysis of X-ray tomograms of sludge during convective drying in a pilot-scale fixed bed
Li, Jie ULiege; Plougonven, Erwan ULiege; Fraikin, Laurent ULiege et al

in Chemical Engineering Science (2015), 134

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See detailInfluence of viscosity on Liquid Flow Inside Structured Packings
Bradttmöller, Christian; Janzen, Anna; Crine, Michel ULiege et al

in Industrial & Engineering Chemistry Research (2015), 54

In this study, X-ray computer tomography and light-induced fluorescence were applied to investigate the morphology of liquid flow inside structured packings. Fluid dynamic parameters such as liquid holdup ... [more ▼]

In this study, X-ray computer tomography and light-induced fluorescence were applied to investigate the morphology of liquid flow inside structured packings. Fluid dynamic parameters such as liquid holdup and wetted surface were determined to study the effect of the variation of viscosity and liquid load. Flow patterns inside the packing were identified and categorized. Liquid film thickness and its distribution were analyzed on single sheets. For both methods, the measured holdup values are in good agreement, despite differences in the techniques of measurement. For the flow patterns and their relative contribution, as well as mean liquid film thickness, a strong dependency on the varied parameters was found. Furthermore, the density function of film thickness distribution changed characteristically with liquid load and viscosity. The complementary use of tomography and optical assessment allowed an improved insight into flow phenomena and the observed interdependency of physical, geometric, and operational parameters. [less ▲]

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See detailInvestigation of the links between mass transfer conditions, dissolved hydrogen concentration and biohydrogen production by the pure strain Clostridium butyricum CWBI1009
Beckers, L.; Masset, J.; Hamilton, C. et al

in Biochemical Engineering Journal (2015), 98

Fermentative hydrogen production has often been described as inhibited by its own gas production. In this work, hydrogen production by Clostridium butyricum was investigated in batch Biochemical Hydrogen ... [more ▼]

Fermentative hydrogen production has often been described as inhibited by its own gas production. In this work, hydrogen production by Clostridium butyricum was investigated in batch Biochemical Hydrogen Potential (BHP) tests and in a 2.5L anaerobic sequenced batch reactor (AnSBR) under different operating conditions regarding liquid-to-gas mass transfer. Through the addition of both stirring up to 400rpm and nitrogen sparging, the yields were enhanced from 1.6 to 3.1molH2molglucose -1 and the maximum hydrogen production rates from 140 to 278mLh-1. These original results were achieved with a pure Clostridium strain. They showed that hydrogen production was improved by a higher liquid-to-gas hydrogen transfer resulting in a lower dissolved hydrogen concentration in the culture medium and therefore in a lower bacterial inhibition. In addition, biohydrogen partitioning between the gas and the liquid phase did not conform to Henry's Law due to critical supersaturation phenomena up to seven-fold higher than the equilibrium conditions. Therefore, dissolved hydrogen concentration should be systematically measured instead of the headspace hydrogen partial pressure. A model was proposed to correlate H2 production yield and rate by the pure C. butyricum strain CWBI1009 with mass transfer coefficient KLa. [less ▲]

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See detailDesigning large-scale CO2 capture units with assessment of solvent degradation
Léonard, Grégoire ULiege; Crosset, Cyril; Dumont, Marie-Noëlle ULiege et al

Poster (2014, October)

Solvent degradation is a major drawback for the large-scale implementation of post-combustion CO2 capture due to amine consumption and emission of degradation products. In the present work, we refine a ... [more ▼]

Solvent degradation is a major drawback for the large-scale implementation of post-combustion CO2 capture due to amine consumption and emission of degradation products. In the present work, we refine a previous kinetic model for describing solvent oxidative and thermal degradation based on experimental results. The CO2 capture process is then modeled in Aspen Plus with assessment of solvent degradation. As a result, this work provides a useful tool for the identification of optimal operating conditions that minimize both the energy and environmental impacts of the process. [less ▲]

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